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新型小麦基连续生物乙醇生产系统的工艺设计与优化

Process design and optimization of novel wheat-based continuous bioethanol production system.

作者信息

Arifeen Najmul, Wang Ruohang, Kookos Ioannis K, Webb Colin, Koutinas Apostolis A

机构信息

Satake Centre for Grain Process Engineering, School of Chemical Engineering and Analytical Science, The University of Manchester, PO Box 88, Manchester M60 1QD, United Kingdom.

出版信息

Biotechnol Prog. 2007 Nov-Dec;23(6):1394-403. doi: 10.1021/bp0701517. Epub 2007 Oct 10.

Abstract

A novel design of a wheat-based biorefinery for bioethanol production, including wheat milling, gluten extraction as byproduct, fungal submerged fermentation for enzyme production, starch hydrolysis, fungal biomass autolysis for nutrient regeneration, yeast fermentation with recycling integrated with a pervaporation membrane for ethanol concentration, and fuel-grade ethanol purification by pressure swing distillation (PSD), was optimized in continuous mode using the equation-based software General Algebraic Modelling System (GAMS). The novel wheat biorefining strategy could result in a production cost within the range of dollars 0.96-0.50 gal(-1) ethanol (dollars 0.25-0.13 L(-1) ethanol) when the production capacity of the plant is within the range of 10-33.5 million gal y(-1) (37.85-126.8 million L y(-1)). The production of value-added byproducts (e.g., bran-rich pearlings, gluten, pure yeast cells) was identified as a crucial factor for improving the economics of fuel ethanol production from wheat. Integration of yeast fermentation with pervaporation membrane could result in the concentration of ethanol in the fermentation outlet stream (up to 40 mol %). The application of a PSD system that consisted of a low-pressure and a high-pressure column and employing heat integration between the high- and low-pressure columns resulted in reduced operating cost (up to 44%) for fuel-grade ethanol production.

摘要

一种用于生物乙醇生产的新型小麦生物精炼设计,包括小麦研磨、作为副产品提取面筋、通过真菌深层发酵生产酶、淀粉水解、真菌生物质自溶以实现营养物再生、结合渗透蒸发膜进行乙醇浓缩的循环酵母发酵,以及通过变压蒸馏(PSD)纯化燃料级乙醇,使用基于方程的通用代数建模系统(GAMS)软件在连续模式下进行了优化。当工厂的生产能力在1000 - 3350万加仑/年(3785 - 12680万升/年)范围内时,这种新型小麦生物精炼策略可使乙醇生产成本在0.96 - 0.50美元/加仑乙醇(0.25 - 0.13美元/升乙醇)范围内。生产增值副产品(如富含麸皮的珍珠麦、面筋、纯酵母细胞)被确定为提高小麦燃料乙醇生产经济性的关键因素。酵母发酵与渗透蒸发膜的结合可使发酵出口物流中的乙醇浓度提高(高达40摩尔%)。由低压塔和高压塔组成且在高低压塔之间采用热集成的PSD系统的应用,可降低燃料级乙醇生产的运营成本(高达44%)。

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